Apparatus for humidifying and cleaning gaseous fluids such as air



Nov. 25, i947. w. L. FLElsHER APPARATUS FOR HUMIDIFYING AND CLEANING GASEOUS FLUIDS SUCH AS AIR Filed Sept. 25, 1945 3 Sheets-Sheet 1 NGV 25, 1947. w. L. FLISHER 2,431,389 l APPARATUS FOR HUMIDIFYING AND CLEANING GASEOUS FLUIDS SUCH AS AIR Filed sept. 25, 1945 5 sheets-sheet 2 ATTORNEYS,

Nov.. 25; 1947, w. L. FLEISHER APPARATUS FOR HUMIDIFYNG AND CLEANING GAsEoUs FLUlDs SUCH As AIR Filed Sept. 25, 1945 3 Sheets-Sheet 3 INVENTOR.

Patented Nov. 25, 1947 APPARATUS FOR HUMIDIFYING AND CLEAN- ING GASEOUS FLUIDS SUCH AS AIR Walter L. Fleisher, New City, N. Y. Application September 25, 1945, Serial No. 618,438

(Cl. 18S-13) 6 Claims.

. This invention relates to means for obtaining intermittent humidirlcation with constant cleaning of air or other gas and for preventing entrainment of droplets or bubbles of the conditioning medium in the gas leaving the conditioner. The apparatus is primarily for wintertime conditioning of houses and other enclosures.

When water, or a combination of water and a viscous fluid such as triethylene glycol, is dumped periodically over the upper part of a sloping filter screen such as a glass filament filter, where purposefully certain portions of the liquid now down the lter or screen for cleaning purposes and other portions pass through the filter or screen for wetting and partial humidiication of the gas passing therethrough, some of the liquid, because of its viscosity and surface tension tends to form itself into minute spheres in the nature of tiny hollow bubbles. These bubbles being very light, are carried along in the air stream and are not taken out by conventional eliminators or hooks, which are commonly an integral part of a washer or scrubber` eliminator, and where the specific gravity of the ordinary water droplets is sufficient for the velocity of discharge to throw the droplets against the surfaces of the eliminator plates. With the tiny viscous bubbles which are developed with a solution such as the solution herein described, there is no tendency for the bubbles to be thrown out of the air stream and consequently a screen having only the nest interstices (such as the filter screen described in Patent No, 2,356,757 or one of similar construction) is effective for the purpose, and even a screen such as this, unless set at the angle herein described, will not effectively remove these bubbles, which are not in the nature of an evaporated vapor.

A principal object of my invention is to provide means for electively eliminating such bubbles or droplets from the gas stream emerging from the device, and only allowing vapors to pass along with the air stream itself.

In the case, for example, where the filter screens are similar to that disclosed in my U. S. Patent No. 2,356,757 or in my co-pending application Ser. No. 549,668, filed Aug. 16, 1944, or with other lilter screens, I have discovered that if a second screen similar in principle to the original filter screen or lter is installed at an angle facing the original screen and approximately at the same angle, the two forming an inverted V, the small bubbles or droplets which ordinarily would be carried over and emitted with the gaseous stream, are eliminated. These small bubbles or droplets are either broken into such small shattered fragments that they attach themselves to and follow the slope of the eliminating screens and are thus carried to the bottom of the screen and to the collecting pan, or else, by the eddy set up by the action of the gas or air stream, because of the angular position of the eliminating screen, are deflected back into the liquid in the collecting pan and thence drained into the liquid medium in the tank.

The velocity of the gas or air stream striking the eliminating screen is of major importance. At the top of this screen where the gas Velocity is greatest, because the distance between the leaving surface of the lter is closest to the entering surface of the leaving eliminator, the eddies created are so strong that they have a tendency to immediately carry the drops or bubbles floating in the gas or air stream away from the entering face of the eliminator to prevent the bubbles or drops from even coming in contact with said face. Also, due to the velocity over this upper surface, I have discovered that an induced current is developed which has a tendency to keep these droplets away from the surface of the leaving screen until they can be absorbed or deflected. In the lower portion of the leaving screen or eliminator where the velocity of approaching gas or air is less, the bubbles or droplets have an opportunity to settle and cling to the face of the eliminator screen, and are then by gravity or gas or air move ment carried to the bottom of the screen and then carried oli to the collecting pan.

If the eliminator screen were not disposed angularly as indicated, namely, so that it and the iilter screen form an inverted V, the structure in section approximating an isosceles triangle with the top apex angle not exceeding degrees, the tendency would be for the droplets to settle on the eliminator screen. They then would eventually work themselves through the latter to again be carried by the emerging air or gas stream as unvaporized droplets. The latter would then become deposited on walls, furniture and ceilings and throughout the ducts and associated apparatus. It isextremely important that this should not occur because the viscous or controlling liquid is expensive and its loss by deposit would require replacement. Moreover, this deposited material would create an undesirable sticky scum on the walls, furniture, ceilings, ducts and associated apparatus. Although these droplets are minute in their individual entities, they constitute a far greater weight oi the viscous material than is actually evaporated and purposefully carried through the leaving screen with the air stream. Consequently, although there. is some danger of the vaporized solution eventually depositing out, it is so minute that it is of no importance, but, if the droplets escape or have a tendency to escape, the effect would be undesirable. Except in true vapor form, none of the conditioningliquid must leave the apparatus.

,Another principal object of this invention therefore is to provide structure meeting the requirements of eliminating scum and loss.

A further object of the invention is to provide simple and effective means for meeting these requirements.

Another principal object of the invention is to provide improved means for securing evenness of flow of the conditioning liquid to theA filtering screen so that uniformity of flow of such liquid over the filtering screen is obtained.

To the accomplishment of the foregoing and such other objects as may hereinafter appear, this invention consists in the novel construction and arrangement of parts, hereinafter to be described in detail and then sought to be defined in the appended claims, reference being had to the accompanying drawing forming a part hereof which shows, merely for the purposes of illustrative disclosure, preferred embodiments of the invention, it being expressly understood, however, that changes may be made in practice within the scope of the claims without digressing from the inventive idea.

In the drawing:

'Fig. 1 is a sectional elevation taken along line I-I of Fig. 2;

Fig. 2 is a sectional elevation taken along line 2-2 of Fig. 1;

Fig. 3 is a transverse section taken along line 3-3 of Fig. 1; and

Fig. 4 is a diagrammatic sectional elevation of a modified form of construction.

Referring to the drawing, I denotes a casing of suitable material that is provided with a gas or air inlet opening H, preferably in its top, and a gas or air discharge opening I2 in one of its sides at the lower portion thereof.

A waterv trough or dumping pan I3, preferably of trapezoidal section is loosely pivoted on shafts I4, I5 between sides of the casing I0, so as to dump or tilt under the weight of a predetermined amount of liquid therein in the clockwise direction of Fig. 1. Suitable abutments I6'. I1 extending from the face of casing Ill, restrict or limit the rotary movement of a crank lever I8 fixed suitably to the pivot shaft I5. The limit stops I5, I1 are fitted with rubber or other sounddeadening material so that in making the dump and returning to normal position the sound of metal to metal between lever I8 and stops I6, I1, is eliminated. These stops prevent over-travel of the dumping pan I3 during dumping of its contents so that it will always return automatically to the normal position shown in Fig. 1 after being emptied. In the embodiment shown, the dump tank I3 is adapted to dump when approximately two gallons of liquid have been delivered to it. This amount, however, is subject to variation as desired.

When the pan I3 is filled to its dumping capacity, it tilts in the clockwise direction of Fig. 1 and delivers its contents so that they strike a baiie plate I9 whence they fall upon the slightly sloping pan 20. In the embodiment shown, the slope of pan 20 is approximately 3A per foot. Both the baiiie plate I9 and sloping pan 2U are suspended suitably within the casing I0. The distance between the bafiie plate I9 and the discharge edge ZliaV of the sloping pan 2D is so admeasured and the time. required for the dumped liquid after it strikes baille plate I9 to reach the discharge edge 20a is sufcient in relation to the viscosity of the dumped fluid to eliminate unevennesses of flow due to impact of the liquid upon the pan 2U, so that substantially absolute uniformity of flow of such liquid over the discharge edge 29a is effected.

A screen-or filter cell 42| is suspended angularly within the container or casing IIl at approximately with the horizontal. The upper edge of this screen or filter cell 2| is positioned to lie directly below the discharge edge 20a of sloping pan 22. The lower edge of the cell 2| extends downwardly and forwardly of its upper edge and rests, for example, on the bracket 22 supported from the casing I0 so as to maintain the desired angular disposition of said cell. This cell 2|, for example, has the construction of the cell of my aforementioned Patent 2,356,757, granted August 29, 1944, or may have other suitable construction.

Asecond cell 23 is suspended within the casing IQ sc that it and the cell 2| in section have the appearance of an inverted V. To this end, the upper edge of cell 23 lies adjacent the upper edge of cell 22, while its lower edge extends forwardly and downwardly and rests, for example, on the bracket 2li supported from the casing Ill and disposed to maintain the angular disposition of cell 23 with respect to cell 2| so that the top or apex angle between the two screens 2| and 23 does not exceed 60. The cell 23 is preferably of similar construction to that of cell 2 I, although it need not be as thick. It also may have other construction if desired.

A collecting member or pan 25 is secured suitably to the bracketv 24. This pan extends the full width of casing I0 between its side walls and has a downwardly sloping portion 25a, a substantially vertical portion 25h and a collecting or sump portion 25e for a purpose to be presently described. This pan 25 also serves as a partitioning member or baffle to force the flow of gas or air from the inlet II through the cells or screens 2| and 23.

The collecting or sump portion 25o slopes downwardly toward one of the side walls of the casing IB to a drain outlet 26 that delivers the collected fluid to a tank 2'| supported suitably from the casing I0.

This tank 21 in the embodiment shown has a capacity of approximately ve gallons, that is, a larger capacity than is required for normal wintertime operation for reasons that will be presently described.

A suitable inlet conduit source of water supply (not shown) and the delivery of water to the tank 2`| from said conduit is controlled by any conventional oat operated valve 29 whose float 30, in the embodiment shown is positioned permanently to cut off water supply to the tank 21 as long as its contents remain above a certain amount to be described. A pump Si of conventional form, driven by a motor 32 is connected with the tank by conduit 33. The delivery conduit 34 of the pump extends upwardly from the pump, terminating in a nozzle 35 overlying the dump bucket I3 so that the liquid pumped from tank 2l is delivered to the said dump bucket or trough I3. If desired, conventional electric circuit connections can be provided to halt operation of the pump While bucket I3 is dumping although this is not essential to successful operation. A conventional drain outlet 36, normally closed by a valve 31 serves to remove the uid from tank 2'I for cleaning thereof or replacement.

The air to be conditioned is circulated by means oi a suitable fan 3B. This fan is positioned Within the casing Iii on a frame 39 so that its discharge outlet i0 discharges air or gas through opening I2 in said casing. The suction inlets 4I 28 is connected to a of the fan open into the casingjl s'oas todrawl air or gas from casing inlet I| through the cells 2| and 23 in the general path indicated bynthe' arrows A of Fig. 1. The fan 38 is driven in con'r ventional manner, for example, by a motor 42- coupled by belting 43 to a sheaveM on the' fan shaft 38a. l K y In a system of air ventilation, where the air is carried through a lter, cell or screen, as screen 21| which is wetted continuously or intermittently by liquid, preferably water, dumping over the top of the screen and owing down the screen, or in a capillary cell, with the' unevaporated water Wasting to the sewer, one of two things is likely to occur. Either too much water is evaporated and too high a relative humidity occurs in the enclosure to which the air is directed', or, if'the water is fed to the tilting pan I3 or other means of intermittent water flow very slowly so that wetting of the screen or cell 2| occursonly 'once or twice an hour, which is all that is ordinarily required for humidication of a well constructed house, the cell or screen is dry for such aleng'th of time; that either the very loosely packed fila; mentsy of the capillary cell or the screens whoseY interstices are small compared to the size of the bubbles and that are relatively large when com'- pared with the average dust particle` no lo'ng'ei` actas good dust elimin'ators or collectors, due to the fact that they are dry andl untreated with adhesive or other compositions, such as are gen-1 erally used in dry filters tocolleot the dust.

To overcome" this condition and to effect addif tional results, I utilize in. combination, a solution of' triethylene glycol and water or other solutions or emulsion, of which water is the lesser part, to eilect the wetting of a slanting cell or screen 2|, the wetting being effected by means of the tilting or unbalanced pan or bucket I3, or other suitable equipment located above the screen 2|.

In a household filter and humidifying appa-Q ratus supplying for example 1300 cubic feetipe'r minute, I have discovered that for thorough washing. and wetting of my filter cell or screen 2| and prop'er'wintertime humidication, at least two gallons of solution must be dumped over a cell or Screen if it is about 25 in length and 20' wide in order to accomplish the thorough scrubbing which is essential for the removal of the dirt reposing on the screen due tothe passage of air; If this liquid is only water, the evapora# tion due to one or two dumps of two gallons per dump is sufficient for humidication purposes;l but as all water reposing on the screens or strands thereof is completely evaporated in a periody of less than four minutes, as a dust arrester the cell or screen is only enicient for a very small pori tion of the total operating period. However, I have discovered that a solution o about 60% to 80% triethylene glycol and 40% to 20% water or other proportions of solutions or emulsions having similar characteristics, which are listed in the paragraph below, when dumped from my tilting pan. I3, will deposita solution. on my screen 2| which is suicient to give about a '40% relative humidity in the wintertime without the danger of overesaturation; while the viscosity of the-solu` tion orv emulsion is suicient to coat the cell laments for a suicient length of time so that the coated strands act as dust collectors during the non-ilushing period of the intermittent flushing" cycle and so that when flushing does occur iuring the prescribed cycle, suflcient aqueous so'- lution is dumped over the cell strands or screenv filaments, to Wash the solution clinging to the have no tendency to harden or crystallize on the iilt'er strands. The percentages of these substances with water will be proportionallto the vapor pressures: of the basic substances and the vapor pressures of the substances-should below so that their'dew pointsV are not below the lowest dew point carried` in the enclosures which would tend to deposit 'out the basic substances on surrounding'walls, ete., causing a feeling of stickiJ- ness. In other words such substances are those that are absorbers but are not readily vaporized; They willj exhibit the characteristics pointed out in the preceding paragraph as to triethylene-glycol and water solution.

Because of the cost of the viscous solution, it is essential to conserve and re-use the solution foi* an indenite period of time. Consequently, the solution which is dumped over the sloping cell or screen is collected on the sloping plate 25dand in sump 25e underneath the screen and drained into the tank 21. This tank 21 must be designed in accordance with this invention to hold from oneLand-a-half' to' twice the Volume of the basis viscous liquidthat is, the triethylene glycol similai liquid chemicall This is an extremely important aspect of this invention; The importance can be understood from a consideration of the operations resulting from use ofthe apparatus.

If the dumping pan I3 or similar equipment holds two gallons essential for proper llushing of the cell or screen 2|, then for winter use the tank 21; must hold at least four gallons of solution so that two Vgallo'nscanv be drawn bypuinp 3| from this tankk and discharged into the dumping pan I3 through conduit 34 and discharge nozzle 35. Ill the tank 27|V which contains the total vdllllhe of solution, the float 30 is positioned to cnt i watei'delivery at the level of' the remainder'left' in the tank 21 after the dumping volume (two iallcll'isY i'n" this ll'ibdll'ellt) is withdrawn. If Water is evaporated during the periodafter a dump,l then on the-nekt filling of the dumping tank A|3 the level remaining in thetank 21 will be retiilicedV below theV cut-off level o f the float 30 and water will flow into the tank 21 to replace theV evaporated water; As the chemicaLsuch as triethyleneglycol or similar viscous material, is minute in its evaporative characteristics, the cimuninoninl the height f liquioin the' tari-k 21 is due primarily'tothe evaporation o f water, and consequently the introduction of additional water when the valve' y29 opens maintains the concentration' in the solution at the right per centag'es tro*maintaintherelative humidities in: dicated. The valve 29- of course. closes as soon as the-float 3,01 rises toits cut-oh level.

On the` other. hand, in the summertimao'r when the dry bulb temperatures rise, the solution of triethylene gli/'oel and water, orv similar solu-` tions,- tensto become a dehydrator, the vapor pressure of the solution changing and water' being absorbed by the Ysolution rather than evapora` tion taking plaee vfr'iin the cfell or screen 2|, In suchv periods, water will be taken up by the'tri: ethylene Fglycol in selution until `a differeritor weaker 'coiie'rlt'aticiiis' developed se that 'with the cut-off setting of the float valve 29.

normal conditions of atr'nospheric pressure, existing, for instance, in the United States, possibly twice as much waterwith the same amount of triethylene glycol or similar solution will be deposited in the tank 21. In order to prevent'the overflow of solution and the loss of the expensive material, the tank 21 must be designed'for, say, ve gallons instead of the four 4which is its normal operating volume in wintertime. However, as the float control valve 29 is set permanently at the winter level, the summertime level in the tank 21 always remains above the cut-off level of the oat 38 and no additional water will Vbe supplied to the solution during this period; In this way, by having the tank 21 designed for the variation in the vapor pressure characteristics of the particular solution, definite humidities can be maintained during the artificially created heating season, and safety facto-rs for the saving of the solution can be maintained during the free Vor mild season. In this way the simplest type of control of humidity is maintained over a wide period of the year without thermostatically sensitive instruments, which respond to the moisture content of the air.

As a small amount of the'triethylene glycol will be evaporated, from time to time the strength of the solution should be tested with a hydrometer,vand the amount of triethylene glycol or' similar solution which has been evaporated should be replaced to bring about the normal conditions for operation and humidication. Ordinarily, a test every two or three months will be suiicient.

If the concentration of the solution has been found to show only a slight decrease due to the slight evaporation of the triethylene glycol or equivalent substance, chemical replacement can be avoided by making only a slight change in Thus it is possible to utilize the apparatus for long periods of time without requiring any replacement of chemical. The actual need for replacement will show up in increased humidity in the air treated,

Normally, the amount of solution which has to be pumped into the tilting pan I3 is of the nature of one-seventh to one-tenth of a gallon per minute in the embodiment shown. Consequently, any small, even inefficient pumping arrangement will supply the necessary flushing action without any appreciable loss in overall efficiency.

. 'I'he equipment described lends itself, by the.

very nature of the characteristics of the solution, to cooling as well as humidication, for when major evaporative cooling is required the supplementary tank 21 can be made still larger in capacity and the strength of the solution reduced to allow of greater evaporation. It is important to bear in mind the two following fundamental characteristics of this invention; although with triethylene glycol and water a perfect solution is obtained, the viscosity of the triethylene glycol holds to the strands of the cell or screen, irrespective of the evaporation or flow of the liquid, and it has the ability of the viscous material to cling during the off period ofv dumping which creates the cleaning which is so essential in the nondumping period. Moreover, the triethylene glycol or other chemical used not only hasthe ability of clinging to the strandsbut of remaining viscous. The nature of the basic substance being an ab,- sorber and taking a condition of equilibrium with the vapor pressure of the moisture of the air coming in contact with it, it will pick up a very slight amount of moisture from the air as the glycol or -similar substance'tends to dry out and then it has reached an vequilibrium it will give up a tiny amount of moisture again to always maintain an equilibrium. In this way without affecting in any material way the condition of the leaving air it remains in a state to pick up the dust throughout the off period and consequently is in itself suiciently unset to be washed oif with its clinging dust particles during the flushing period. This property is of great importance because itis apparent that cleaning is enhanced by a substance Whichretains its viscosity.

As has been stated at the outset of this specification, because of its viscosity and surface tension, some ofthe liquid, tends to form itself into minute spheres, in the nature of tiny hollow bubbles, that are carried along by the air or gas stream flowing through filter screen 2|. However, these bubbles or drops are eliminated effectively by the second or eliminator screen 23. These small bubbles or droplets are either broken into such small, shattered fragments by the screen 23 that they attach themselves to and follow the slope of the said eliminating screen 23 and are thus carried to its bottom and fall onto the collecting pan 25, or else by the eddy set up in the space' formed by the screens 2| and 23, because of the angular position of the eliminating screen 23 are deflected directly into the collecting pan 25 and drained into the liiquid medium in tank 21. The ordinary eliminator with hooks has a free area of anywhere from 1/2" to 11/2, and the only reason droplets are caught is due to the change of direction of the airflow. The droplets, for instance, of water, having a greater density than the air, project themselves into the hooked spaces. As the droplets of the viscous material are probably not over 116" in diameter, of course they would not be affected by the ordinary eliminators but would float through the spaces through which the air passes without being projected into the hooked receiving spaces.

The velocity of the gas or air stream striking the eliminating screen 23 is of major importance. At the top of this screen where its entering surface is closest to the leaving surface of the lter 2|, the air or gas velocity is greatest and the eddies created are so strong that they have a tendency to immediately carry the drops or bubbles floating in the air or gas stream emerging from the leaving surface of filter 2| away from the entering face of the eliminator screen 23 to prevent the bubbles or drops from even coming in contact with said face. At the lower portion of the eliminator screen, where the velocity of the approaching gas or air is less, because of greater distance from the leaving surface of filter screen 2|, the bubbles or droplets in the air approaching the entering surface of the eliminator screen have an opportunity to settle and cling t0 such entering face. Then by gravity, or by gas or air movement, such drops or bubbles are carried to the bottom of the screen 23 and are then moved ofi.' onto the collecting pan 25 and thence to tank 21. The angular disposition of the eliminator screen 23 so that it with the filter screen 2| forms an inverted V whose apex angle does not exceed 60 is of utmost importance. Unless such construction is utilized the tendency would be for the drops or bubbles to settle on the eliminator screen 23 and eventually'work themselves through the latter to again Ybe carried in the air or gas stream delivered through outlet 2, there appearing as unvaporized droplets which would eventually cover walls of theenclosure conditioned with a sticky scum. The eliminator screen 23 and its arrangement relative to iilter screen 2| obviates such an occurrence. Only a very small part of the viscous material of the conditioning liquid is vaporized which either is not noticeable or is eliminated by the ordinary exltration of air from the enclosure.

The principles disclosed can be adapted for use with a multiple cleaning and humidifying apparatus as is illustrated diagrammatically in Fig. 4. Therein the dumping trough I3' discharges its contents to deliver the conditioning liquid to the lter screen 2|. The liquid drained therefrom and the eliminated bubbles or droplets from its eliminator screen 23' are caught on the drain pan 25. This pan 25' is controlled by a weighted gate 59. When the liquid collected in the sump portion 25'cof the pan 25 overcomes the weight 5 I, the sump contents are dumped to cascade over the second filter screen 2l". The liquid drained from the latter screen and the eliminated bubbles and droplets from its eliminator screen 23" are caught on drain pan 25". This pan is likewise controlled by a weight operated gate 50'. When the liquid collected in sump portion 25c of the pan 25 overcomes weight 5I', the sump contents are dumped to cascade over the next succeeding iilter screen 2V" also having associated with it an eliminator screen 23". Ultimately the residual liquid is returned to a collecting tank for repumping to the original dump trough I3. It will be noted that each lter screen and its associated eliminator screen forms an inverted V whose apex angle does not exceed 60. The number of such sets of inverted Vs can be as desired. The principle of operation whether a single set or multiple sets are used is the same as that described for the single set of Figs. 1 3, incl.

rThe apparatus described may be used directly for conditioning a room or enclosure. It may also, for example, be used in conjunction with a heating system, such as a warm air heating system, as described in my co-pending application Ser. No. 549,668. When so used, the casing i0 and its contents may be positioned adjacent to the hot air L furnace. An air inlet conduit for leading air from the outside of the house is connected to the inlet il of casing lo. The delivery outlet l2 of the casing is connected by a conduit to the air inlet of the furnace so that conditioned air from the device of the invention is delivered to the furnace, heated therein and from the latter is delivered by conduits to the room or rooms of the house. Ordinary heating or cooling coils such as those used for hot water or steam heating can be inserted in the discharge outlet |'2 from the fan and the apparatus used, therefore, for any type of heating.

While specio embodiments of the invention have been disclosed, it is to be understood that changes may be made in practice and are contemplated. The size and dimensions of the devices are not to be construed as limited to those described as they may be varied in practice to suit dinerent operating requirements. There is no intention of limitation to the exact details shown and described.

What is claimed is:

1. In apparatus of the character described, gas cleaning and humidifying means, means for dumping a predetermined quantity of conditioning liquid, a baille positioned to receive the initial impact of the dumped uid and a pan serving thereafter to receive the said fluid and to deliver it at a point remote from said baille to said gas cleaning and humidifying means, the distance between said baille and the delivery point being admeasured so that sufficient time elapses in relationship to the viscosity of said liquid as to eliminate uneveneness due to impact of the liquid on said pan and to permit said liquid to level out and ow uniformly to the said gas cleaning and humidifying means at said delivery point.

2. In apparatus of the character described, a filtering or conditioning screen, means for periodically dumping a predetermined quantity of conditioning liquid, a baille positioned to receive the initial impact of the dumped liquid, and a pan joined to saidbaiile and onto which the said liquid is denected from said balile, said pan sloping from its junction with said baille to a delivery point arranged over the upper edge of said screen, the said delivery point being remote from said baiile and adineasured in distance therefrom so that suicient time elapses in relationship to the viscosity of said liquid as to eliminate unevenness caused by impact of the liquid on said pan and to permit said liquid to level out and flow uniformly to said screen at said delivery point.

3. Apparatus for conditioning a gaseous uid such as air under wintertime conditions in an enclosure wherein the fluid is largely recirculated to a prescribed humidity and for cleaning thereof, comprising a casing having an inlet for such uid in its top and an outlet for the conditioned uid in one of its sides in a lower portion thereof, a tank for a glycol-water containing solution of desired concentration supported by said casing, a conduit for connecting said tank to a source of water supply, a float-operated valve in said con- '4 duit, a float for operating said valve, a tiltable trough positioned in said casing above the level of said tank and adapted to tilt to a dumping position under the weight of a prescribed amount of Said solution delivered thereto, means for pumping said solution from said tank to said trough, a plate member onto which the prescribed amount of solution in said trough is dumped periodically with each tilting of said trough, a ltering screen positioned within said casing at an angle with the horizontal and below said plate member onto which the solution dumped onto said plate member falls, a collecting trough having a sloping bottom positioned below said screen to catch the portions of the solution falling from said screen, an eliminating screen positioned within said casing at an angle to said iiltering screen and below said plate member, and means to return such solution portions from said collecting trough to said tank, said iioat being positioned to operate said valve to cutoif at the level of the remainder of initial solution in said tank just after the rst prescribed dumping amount has been pumped therefrom to said dumping trough, and to permit said valve to open whenever the solution in said tank is below such level whereby replenishment of water evaporated from the solution in its travel from dumping trough back to said tank will be effected to restore the desired glycol-water solution concentration, and a fan within said casing for drawing the fluid to be conditioned through said inlet and through said ltering screen and for thereafter blowing the conditioned fluid outwardly through said casing outlet.

4. Apparatus for conditioning a gaseous fluid such as air under wintertime conditions in an enclosure wherein the iiuid is largely recirculated to a prescribed humidity and for cleaning thereof, comprising a casing havingv an inlet for such fluid in its top and an outlet for the conditioned fluid in one of its sides in a lower portion there- V1.1 of, a tank for a glycol-water containing solution of desired concentration supported by said casing, a conduit for connecting said tank to a source Vof water supply, a float-operated valve in said conduit, a iioat for operating said valve, a tiltable trough positioned in said casing above the level of said tank and adapted to tilt to a dumping position'under the weight of a prescribed amount of said solution delivered thereto, means for pumping said solution from said tank to said trough, a plate member onto which the prescribed amount of solution in said trough is dumped periodically with each tilting of said trough, a filtering screen positioned within said casing below said plate member ontorwhich the solution dumped onto said plate member falls, a collecting trough positioned below said screen t-o catch the portions of the solution falling from said screen, an eliminating screen positioned within said casing at an angle to said iiltering screen and below said plate member, and means to return such solution portions from said collecting trough to said tank, said float being positioned to operate said valve to cut-off at the level of the remainder of initial solution in said tank just after the first prescribed dumping amount has been pumped therefrom to said dumping trough, and to permit said valve to open `whenever the solution in said tank is below such level whereby replenishment of water evaporatedr from the solution in its travel from dump ing trough back to said tank will be effected to restore the desired glycol-water solution concentration, a fan within said casing for drawing the fluid to be conditioned through said inlet and through said ltering screen and for thereafter blowing the conditioned fluid outwardly through said casing outlet,-and said tankhaving a capacity which is approximately 25% in excess of the required volume of said glycol-water containing solution for wintertime air conditioning.

5. Apparatus for conditioning a gaseous fluid suchas air under wintertime conditions in an enclosure wherein the uid is largely recirculated to a prescribed humidity and for cleaning thereof, comprising a casing having an inlet for such iiuid in its top and an o'utlet for the conditioned uid in 'one of its sides in a lower portion thereof, a tank Yfor a glycol-water containing solution of desired concentration supported by said casing,va conduit for connectingsaid tank to a source of water supply, a float-operated valve in said conduit, a float for operating said valve, a tiltable trough positioned in said casing above the level of said tank and adapted to tilt to a dumping position under the weight of a prescribed amount of said solution delivered thereto, means for pumping said solution from said tank to said trough, a plate member onto ywhich the prescribed amount of solution in said trough is dumped periodically with each tilting of said trough, a filtering screen positioned within said casing below said plate member onto which the solution dumped onto said plate member falls, a collecting trough positioned below said screen to catch the portions of the solution falling from said screen, an eliminator screen positioned Within said casingat an angle not exceeding 60 with said ltering screen to form an inverted Vy construction and below said plate member, and means to return such solution portions from said collecting trough to said tank, said float being positioned to operate said valve to cut-oli at the level of the remainder of initial solution in said tank just after the rst prescribed dumping amount has been pumped therefrom to said dumping trough, and to permit 12 said valve to open-whenever, the solution 1n said tank is belowsuchlevel.whereby replenishment of waterfevaporated 'from the solution in its travel from dumping trough* back to said tank willbe effected to restore the desired.glycol-waterV solution concentration, a fan within said casingfor drawing the iiuid to .be conditioned through said inlet and through said iiltering screen and for thereafter blowing the conditioned iiuid outwardly through said casing outlet, and said tank having a capacity which is substantially greater than the volume of said glycol-water containing solution required for wintertime air conditioning to prevent loss of solution by overflow from the tank whenever operation of the device is continued in milder seasons of the year.

6. Apparatus for conditioning a gaseous fluid such as air under wintertime conditions in an enclosure wherein the uid is largely recirculated to a prescribed humidity and for cleaning thereof, comprising a casing having an inlet for such fluid in its top and an outlet for the conditioned fluid in one of its sides in a lower portion thereof, a tank for a glycol-water containing solution of desired concentration supported by said casing, a conduit for connecting said tank to a source of water supply, a float-operated valve in said conduit, a float for operating said valve, a tiltable trough positioned in said casing above the level of said tank and adapted to tilt to a dumping position under the weight of a prescribed amount of said solution delivered thereto, means for pumping said solution from said tank to said trough, a plate member onto which the prescribed amount of solution in said trough is dumped periodically with each tilting of said trough, a filtering screen positioned within said casing below said plate member onto which the solution dumped onto said plate member falls, a collecting trough positioned below said screen to catch the portions 'of the solution falling from said screen, an eliminator screen positioned within said casing at an angle not exceeding 60 with said iiltering screen to form an inverted V construction and below said plate member, and means to return such solution portions from said collecting trough to said tank,

'said Viioat being positioned to operate said valve to cut-off at the level of the remainder of initial solution in said tank just after the first prescribed vdumping amount has been pumped therefrom to said dumping trough, and to permit said valve to open whenever the solution in said tank is below such level whereby replenishment of water evaporated from the solution in its travel from dumping trough back to said tank will be effected to restore the desired glycol-water solution concentration, and a ian within said casing for drawing the fluid to be conditioned through said inlet and through said filtering screen and for thereafter blowing the conditioned fluid outwardly/through said casing outlet.

WALTER L. FLEISHER.

REFERENCES CITED The following references are of record in the iile of this patent:

UNITED STATES PATENTS Number Name Date 494,264 Seymour, Jr Mar. 28, 1893 1,042,864 Winks Oct. 29, 1912 1,988,262 Burekhalteret a1. Jan. 15, 1935 2,137,905 Church et al Nov. 22, 1938 2,197,004 -Meyers Apr. 16, 1940 2,356,757 Fleisher Aug. 29, 1944 

